The invention relates to a dryer for the treatment of garden waste, so called lop, as well as further bulk material, e.g. chips.
A great number of dryers have become known for drying of any kind.
E.g. dryers have become known, comprising a container with a double bottom. Thereby, a first bottom is arranged above the other one. The upper bottom is perforated. Drying air is fed through the perforations into the space above the first bottom. A disadvantage consists in the fact that drying is not effected uniformly so that there is a humidity gradient in the material.
Further, there are belt dryers. Thereby, material to be dried is deposited on a conveyer belt, and air is blown onto it, e.g. coming from above or from below. Again a material is produced the humidity of which is different at different locations so that there is a humidity gradient. Also, the dimensions of such belt dryers are very large. Particularly with chips of wood the belt is not covered uniformly.
Drying towers have become known, comprising a tower shaped container. The material is fed to the container from above, and removed from below. Thereby, the stream of drying air is not always uniform. Also, there is the risk of clogging.
With drum dryers the material is fed into the drum at one side, and removed at another one. Also, air is blown into the dryer. The air transports the light wood particle toward the exit so that the dwell times become short, or complicated inserts are necessary which jeopardize maintenance, and tend to clogging. A further disadvantage consists in that the dwell times during drying are different from particle to particle. The drum dryer does not operate economically at lower temperatures. Therefore, it has to be very large.
Further, fluidized bed dryers have become known, whereby a fluidized bed is formed by the material to be dried. In case of a material the particles of which have a certain weight, or have the tendency to intermingle, such as wood chips, there is no perfect mixing. Therefore, drying is not uniform.
The material mentioned above, e.g. garden waste etc., is particularly problematic. This is particularly true if the material comprises fibrous or thread like particles having a tendency to spinning. Thereby, balls are formed which form clusters. The inner area of such clusters is not sufficiently dried, but remains humid.
It is the objective of the invention to provide a dryer which is simple in design, produce uniform drying, allows for long dwell times at low volumes, and may be manufactured a low costs. The dryer should be particularly suitable for drying of the material as mentioned above.
The said objective is solved by the features of claim 1.
Accordingly, a dryer according to the invention comprises the following features:
The container may have the form of a shell or a tub open at its upper end. It may be closed, such as a cylinder. It may have a circular cross section or an elliptical cross section, or any other cross section. It is important that the bottom area is at least partially round.
The inventors have perceived the following:
In case further conveying means are used, located in the container and rotating the material on its way from inlet to outlet of the container, there is the risk of compression of the material. Such compressing is extremely disadvantageous. There is the risk of locking of the conveyer means, i.e. of a rotating stirrer. Further, the material is not distributed uniformly, because forming of the said clusters is enhanced. There remains humidity inside of each cluster. Therefore, the drying is not uniform. This is particularly the case if a stirrer is used, comprising a stirrer shaft which is arranged parallel to the conveyer path inside the container, further stirrer arms which when rotating in the descending quadrant of the container wall exert pressure onto the material, thereby compressing the same.
If, however, instead the material is guided along the container wall over a certain distance in the ascending quadrant of the container wall upwardly, it will tip over to the centre of the container. Thereby, a rotating movement of the material is achieved. The material conducts two movements: First, a travelling movement from inlet to outlet of the container, and second the said rotating movement. Compression of the material is avoided.
Various conveying elements may be considered. See the description of the figures.
It is advantageous to locate pressurized air used for drying and loosening in the ascending quadrant of the container wall. This may enhance the rotary movement of the material.
Also, a plurality of pressurized air jets may serve as conveying means so that no (mechanical) conveying means are necessary.
Instead of the said conveying means located in the ascending quadrant, or in addition to those, also the following solution may be considered: Pressurized air is fed primarily or alone in the ascending quadrant of the container wall. A stirrer may be provided. The same should preferably comprise stirrer arms, which are curved so that the same in a certain sense envelope put the material into rotation. Thereby the mass of material is located in the ascending quadrant of the container wall.
The invention is explained by the drawing, showing the following in greater detail:
The first embodiment as shown in
The container comprises a stirrer 3, with a stirrer shaft 3.1 and stirrer arms 3.2. As may be seen from
The curvature of the stirrer arms 3.2 serve the following purpose: The pressure which any stirrer arm during rotation exerts onto the material, is minimized, and therewith also blocking up and forming of clusters of the material.
The material 5 is collected in the region of the ascending quadrant of the container wall. It follows a rotational movement. See both arrows 6. The ascending quadrant acts as kind of a rotating bed. The embodiment shown in
With the third embodiment shown in
Of particular importance is the fourth embodiment as per
In general, the pressurized air with all embodiments preferably is fed to the ascending quadrant of the container wall. It may, however, outside of the said quadrant be fed through additional perforations.
The dryer according to the fifth embodiment as per
Below the first container 1 there is a second container 10. It is approximately as long as the first container, in the present case somewhat shorter. The second container 10 also comprises one or several connections 10.1 as air inlets.
Between the two containers 1 and 10 there is an intermediate wall 20. Intermediate wall 20 is common to both containers 1 and 10, thereby separating the same. Intermediate wall 20 comprises a plurality of perforations 20.1.
The second container 10 is of conical cross section. It is provided with removal means. Inside the second container 10 there are conveying means as removing means, such as a screw conveyer 11. At the end of screw conveyer there is an outlet 11.1.
The dryer according to
During operation of container 1 the material 5 will adopt a certain level.
With this as well as with all other embodiments the speed of the stirrer 3 is adjustable. Also an intermitting mode of operation may be considered.
The first container at its downward end comprises an overflow weir 1.5.
The following features respectively steps may be advantageous with all embodiments:
The dryer according to the fifth embodiment may perform the following operations—see particularly the embodiment according to
The treated material is dry and free of undesired components. It may be processed to pellets or briquettes. It may be burned directly. Also the use with pyrolysis processes may be considered.
Invention may be summarized as follows:
Number | Date | Country | Kind |
---|---|---|---|
10 2009 010 003.2 | Feb 2009 | DE | national |
10 2009 051 381.7 | Oct 2009 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
---|---|---|---|---|
PCT/EP2010/001009 | 2/18/2010 | WO | 00 | 7/8/2011 |